Title: Flow Measurement Some Basic Terms and Concepts
1Flow MeasurementSome Basic Terms and Concepts
- Fluid - The state of a substance in which its
particles easily move and change their relative
position without a separation of the mass and
that easily yield to pressure. A fluid can be a
liquid (generally considered incompressible) or a
gas. - Mass - Quantity of matter that causes it to have
weight in a gravitational field. Mass flow is
expressed in weight/time, ie kilograms/hr. - Volume - Space occupied or enclosed by cubic
units. Volumetric flow is expressed in cubic
measure/time i.e. cubic feet/minute or
gallons/hour. - Density - Mass of a substance per unit volume.
- Specific Gravity - The ratio of the density of a
substance to the density of some some substance
taken as a standard. For flow of liquids,
specific gravity of fluid is compared against
that of water, for gases against that of air. - Mole - grams/molecular weight
- SCFM - Standard Cubic Feet per Minute.
2Flow MeasurementSome Basic Terms and Concepts
- Liquids are generally considered incompressible
- Ideal Gas Law - The pressure, temperature and
volume of a gas are all interrelated. - PV nRT
- P pressure of the gas
- V the volume that the gas occupies(ie ft3)
- n number of moles
- R ideal gas constant (a universal constant)
- T temperature of the gas in absolute units
- For the gas industry flow is most commonly
measured as volumetric flow and expressed at base
conditions - volume is dependant on temperature and pressure
and composition - volumetric measurement must be corrected back to
base conditions - usually 60 - 700F and 1 atmosphere (14.73 psia)
pressure
3The Object of Flow Measurement
- How much went from one place to another?
- Volumetric
- corrected to base pressure and temperature
- Mass
- Mass is mass. It doesnt change with changes in
temperature or pressure.
4A Variety of Flow Measurement Methods
- Orifice plate meter
- Most common in the gas industry
- Relatively low rangeability
- Least accurate of all popular methods
- High installation cost
- No moving parts low (or no) maintenance
- No calibration little maintenance
- Intrusive device
5Orifice Plate Meter
Differential Pressure
6A Variety of Flow Measurement Methods
- Turbine Meter
- Most common meter type across all industries
- Second most common in the gas industry
- Much more accurate than orifice plate
- Wide flow rangeability
- Low relative cost to purchase but comparatively
high cost to maintain - Has moving parts that can fail but is easily
field repaired - Requires calibration
- Intrusive device
7Turbine meters
- Use a vaned rotor engaged by the flowing fluid
- the fluid spins the rotor at an angular velocity
proportional to the flow rate - As the turbine rotates, an AC voltage is induced
in a magnetic pickup - mounted externally to the fluid process
- As each turbine blade passes the pickup the total
magnetic flux density is changed - induces a single voltage pulse
- Each pulse represents a finite volume of fluid
that has been displaced through 2 adjacent rotor
blades.
8A Variety of Flow Measurement Methods
- Positive displacement meter
- Most accurate
- Uses standard low speed digital input on PLC
- Other less common types
- Venturi meter
- Ultrasonic meter
- Vortex meter
- Lots more
9Flow Measurement by the Orifice Plate Method
- Origins of the fluid flow Laws
- More than 300 years ago, Charles and Boyle
discovered that - Uf1 (P h)1/2
- The formula looks deceptively simple
- Qb (218.573Cd(FT)EvY1d2Tb/Pb)(Pf1Zb Zb
airhw/GiZf1Tf) ½ - And it would be,
10Flow Measurement by the Orifice Plate Method
- Origins of the fluid flow Laws
- More than 300 years ago, Charles and Boyle
discovered that - Uf1 (P h)1/2
- The formula looks deceptively simple
- Qb (218.573Cd(FT)EvY1d2Tb/Pb)(Pf1Zb Zb
airhw/GiZf1Tf) ½ - And it would be, except each component of the
equation,
11Flow Measurement by the Orifice Plate Method
- Origins of the fluid flow Laws
- More than 300 years ago, Charles and Boyle
discovered that - Uf1 (P h)1/2
- The formula looks deceptively simple
- Qb (218.573Cd(FT)EvY1d2Tb/Pb)(Pf1Zb Zb
airhw/GiZf1Tf) ½ - And it would be, except each component of the
equation, for example the Coefficient of
discharge term, relies on solving an equation
like this
12Flow Measurement by the Orifice Plate Method
- Origins of the fluid flow Laws
- More than 300 years ago, Charles and Boyle
discovered that - Uf1 (P h)1/2
- The formula looks deceptively simple
- Qb (218.573Cd(FT)EvY1d2Tb/Pb)(Pf1Zb Zb
airhw/GiZf1Tf) ½ - And it would be, except each component of the
equation, for example the Coefficient of
discharge term, relies on solving an equation
like this - Cd(FT) Ci(FT).000511(106 ß/Red)0.7((0.0210.004
9(19,000ß/ Red)0.8) ß4(106/ Red)0.35
13Flow Measurement The Names and Numbers to Know
- For measuring flow there are 3 equations that are
the most common - For orifice plate meters, AGA 3
- 1992 version
- 1985 version
- ISO 5167 is equivalent and is very similar
- ISO is currently upgrading and will probably come
into lock step with AGA - For turbine meters AGA 7
- AGA 7 is a relatively simple equation compared to
AGA 3 -
- Uf1 (f/K)M
14Flow Measurement The Names and Numbers to
Know(contd)
- For high accuracy gas measurement a
compressibility and sometimes supercompressibility
equation is needed - AGA 8 Most common
- 2 versions
- 1985
- 1992(ISO12213)
- Multiple methods
- Gross methods
- 2 for 1992 (recommended method for use between 32
to 130 oF and less than 1,200 psia, provided the
gas composition is within the normal range) - 4 for 1985
- Detailed methods
- 1992 is the most accurate and most common
15Flow Measurement The Names and Numbers to
Know(contd)
- Other compressibility equations(in order of
popularity) - NX-19 (developed in 1962)
- Still used frequently in high C02 applications
- Compressibility equations used for special gas
compositions - Soave Redlich Kwong (SRK)
- Wichert Aziz
16Flow Measurement The Names and Numbers to
Know(contd)
- API 2540
- Used for liquid measurement with turbine or
rotary displacement meters - Provides temperature and pressure compensation
17Flow MeasurementPutting it all Together
- For measuring gas with an orifice plate meter use
one of these - AGA 3 alone
- AGA 3 with AGA 8
- AGA 3 with NX-19
- AGA 3 with other
18Flow MeasurementPutting it all Together (Contd)
- For measuring gas with a turbine meter
- AGA 7 alone
- AGA7 with AGA 8
- AGA7 with NX-19
- AGA7 with other
19Flow MeasurementPutting it all Together (Contd)
- For measuring liquid with an orifice plate meter
- AGA 3 alone
- For measuring liquid with a turbine meter
- AGA 7 alone
- AGA 7 with API 2540
- For measuring liquid with a rotary displacement
meter - API 2540
20Flow MeasurementAPI 21.1 Audit Trail and Event
Log
- Custody transfer applications are those where the
fluid being measured changes ownership at the
meter point - If the measurement application is not custody
transfer it is - Allocation (often requires API 21.1 for
convenience) - Control
- For custody transfer applications a detailed
audit trail and event log are required - The Industry expects a minimum of
- 7 days of hourly averages of specified variables
- 35 days of daily averages of the same variables
- A copy of the configuration of the meter
parameters - A 100 entry time stamped log of events
- All parameter changes
- Alarms
21Flow MeasurementIf You Dont Know for Sure, Just
Ask
- If a customer says he needs an RTU that does AGA
that doesnt mean anything! - Ask the customer some basic questions and consult
your notes. - What is being measured?
- What kind of meter do they have?
- How accurate does the measurement need to be?
- Is the customer doing custody transfer?
- If a customer is just doing control based on flow
measurement - AGA 3 or 7 alone are often accurate enough.
22What is the Market for Flow Meters
- Orifice Plate Meters
- New installations projected to be
- mil.
- Revenues bil. Increasing by annually through
2002 - Turbine Meters
- New installations projected to be
- Revenues mil. Increasing by annually through
2002 - Source Frost Sullivan Worldsearch May,1996
Under Construction
23What does Schneider offer?Orifice plate meters
- Starling Associates Gas Flow Loadable Function
Block Library - To run loadables on a continuous basis you must
use the proper enabler, 130 HEK 301 01 or 130 HEK
301 02 - Fits in the bus expansion port of a Compact or
Micro PLC. - Disallows the use of the AS HDTA 202 2 slot rack.
- Must be used with a IA WBXT 204 cable if an AS
WBXT 201 is used. - Loadables can be run, without an enabler, in demo
mode for 48 hours after program load.
24What does Schneider offer?Orifice plate meters
(continued)
- Starling Associates Gas Flow Loadable Function
Block Library - consists of 5 blocks that cover the different
calculation combinations
- G392 - up to 8 meters of AGA 3 1992 alone. API
21.1 audit trail - GD92 - meter of AGA 3 1992 and AGA 8 detailed
method. - GFNX - up to 8 meters of AGA3 1985 and NX-19.
API 21.1 audit trail - GG92 - up to 8 meters of AGA 3 1992 and AGA 8
both gross methods. API 21.1 audit trail - GM92 - up to 8 meters of AGA 3 1992 and AGA 8
detailed method. API 21.1 audit trail
25What does Schneider offer?Orifice plate meters
(continued)
- Flow calculations run only on Compact and Micro
612 04 CPUs - Except for the 612 04 you must have a minimum of
16K 984 LL capable CPU to run GG92, GFNX or GM92 - The 612 04 is a special case which can run any of
the flow loadables and have a large amount of
program space left. - GD92 and G392 may be run in as small as a Compact
141 CPU - Using these loadables in an 8 K controller leaves
little space for other programming.
26What does Schneider offer?Turbine meters
- AS BVRC 200, AS BCTR 205 and AS BCTR 224
- High speed counter input cards, for the Compact
and Modicon Micro, that perform the AGA 7
Calculation in the module - K and M factors are configured in the module
and a corrected count or rate is delivered to the
CPU. - BVRC 200 takes direct turbine meter sine
frequency input signal - BCTR 205 and 224 take square wave DC input
signals, 5 VDC and 24VDC respectively. - API 2540 temperature compensation and pressure
compensation is currently not supported as a
solution but can be programmed by the end user.
27What does Schneider offer?Orifice plate meters
(continued)
- Flow calculations run only on Compact and Micro
612 04 CPUs - Except for the 612 04 you must have a minimum of
16K 984 LL capable CPU to run GG92, GFNX or GM92 - The 612 04 is a special case which can run any of
the flow loadables and have a large amount of
program space left. - GD92 and G392 may be run in as small as a Compact
141 CPU - Using these loadables in an 8 K controller leaves
little space for other programming.